a spr sensorgrams for different concentrations of glyphosate 0 2 4 8 16 32 and

Efficient progressive collapse analysis for robustness evaluation and enhancement of steel concrete composite buildings

... such as ABAQUS (ABAQUS, 20 0 5) and LS-DYNA (Hallquist, 20 0 6) Some notable studies adopting detailed FEA include the work by Alashker et al ( 20 1 0), Kwasniewski ( 20 1 0), Yu et al ( 20 1 0), Fu ( 20 0 9) and ... (e.g Aceh 20 0 4, Sichuan 20 0 8, Christchurch 20 1 0- 20 1 1 and Tohoku 20 1 1) and other natural hazards (e.g tsunami, flood and typhoon) have constantly reminded us of the importance of preparing for unforeseen ... check, alongside other permanent loads Partial load factor of 1 .05 and 0. 90 should be used for permanent loading adding to adverse and beneficial effect (BSI, 20 0 0) For members that fail to satisfy...

244
923
0

An Introduction to Intelligent and Autonomous Control-Chapter 5: Modeling and Design of Distributed Intelligence Systems

Danh mục: Quản trị Web

...

19
645
1

Tài liệu Design of Feedback Control Systems for Stable Plants with Saturating Actuators ppt

Danh mục: Cao đẳng - Đại học

... 10 10] T 100 .00 70. 00 mp 40 . 00 ¢.- 10. 00 - 20 . 00 - 50. 00 0 .00 1 .00 2 .00 3 .00 4 .00 5 .00 Time (sec.) Figure 4 .22 : Controls in the F8 system with saturation and the EG, (r = [ 10 10] T) Page 36 AX for ... for the F8 closed loop vith r=[ 10 ] T (t) 1. 10 0 .88 0. 66 0. 9 A( t) 0. 6 0. 44 0. 3 0. 22 0. 0 0. 0 0. 15 0. 30 0 .45 0. 60 0.75 0. 00 0 .00 1 .00 2 .00 3 .00 4 .00 5 .00 Tiwme (sec.) Figure 4 .23 : X(t) in the F8 ... system with saturation, (r = [.3 3]T) Page 25 Academic example vith saturation 4 .00 3 .00 2 .00 2' 1 .00 0. 00- -1 .00 0. 00 2 .00 4 .00 6 .00 8 .00 10. 00 Time (sec.) Figure 4. 9: Output response for the system...

39
595
0

Báo cáo khoa học: Insights into the design of a hybrid system between Anabaena ferredoxin-NADP+ reductase and bovine adrenodoxin pot

Danh mục: Báo cáo khoa học

... d ) 325 ) 305 )33 8a )31 2a )31 2a )29 8a ) 305 ) 28 /b> 6 ) 3 02 /b> ) 307 ND )318f )29 9f )315f ) 320 f ND ) 28 /b> 2f )27 3f ) 28 /b> 9f )29 4f ND ) 305 )3 18 )29 2 2. 7 0. 5 NR d 15 .2 1 46 /b> d 1 60 d 100 a Data from [13,31] b kobs values ... form Adxoxb Fdoxc Adxrdb WT K75E 0. 003 0. 01 d < 0. 001 NR NR L76S L78S L78D L78F L78V 0. 01 0. 005 0. 01e 0. 02 0. 035 NR 0. 41 0. 03 2 40 > 60 0 0. 0 14 0. 0 12 0. 01 0. 01 NR V136S 0. 03 NR Fdrdc Eox/rda (mV) ... the appearance of the typical absorption spectrum of the CO-ferrous CYP1 1A1 complexed form, characterized by absorbance decreases at 3 90, 4 30 and 4 80 nm and by the appearance of a peak at 45 0...

10
400
0

Báo cáo khoa học: "User studies and the design of Natural Language Systems" doc

Danh mục: Báo cáo khoa học

... told them that an English interface to a database was run3.1 Preliminary analysis and filtering ning on the machine and that the database contained information about paintings by Van Gogh and other ... Guida and G Mauri A formal basis for performance evaluation of natural language understanding systems American Journal of Computational Linguistics, 10: 15 -29 , 19 84 In COLING 88: Proc l~th International ... such as spreadsheets or graphics packages Of the remainder, had some experience with using databases and one of these had participated in the design a database None of them was familiar with the...

8
393
0

surface production operations - design of oil handling systems and facilities

Danh mục: Hóa học - Dầu khí

... Media 6 20 Summary of Filter Types 6 20 Removal Ratings 62 1 Nominal Rating 62 1 Absolute Rating 62 2 Beta ( ) Rating System 62 3 Choosing the Proper Filter 6 24 /b> Nature of Fluid 6 24 /b> Flow Rate 62 5 Temperature ... possible Library of Congress Cataloging-in-Publication Data Application submitted British Library Cataloguing-in-Publication Data A catalogue record for this book is available from the British Library ... Operations 48 /b> 3 Onshore Operations 48 /b> 4 Characteristics of Produced Water 48 /b> 4 Dissolved Solids 48 /b> 4 Precipitated Solids (Scales) 48 /b> 5 48 /b> 5 Calcium Carbonate (CaCO3 ) 48 /b> 5 Calcium Sulfate (CaSO4 ) 48 /b> 6...

747
1,141
0

Báo cáo hóa học: " Optimal Design of Noisy Transmultiplexer Systems Huan Zhou1 and Lihua Xie2" docx

Danh mục: Báo cáo khoa học

... crosstalk constraint Band 23 .27 97 4. 1931 32 .03 17 5 .83 82 48 /b> .9 783 5. 544 8 Band 30. 89 80 11. 64 30 33 .8 1 04 /b> 12. 223 8 76. 1 100 6. 68 3 5 SNRc = 20 dB Band 26 /b> .1 188 9 .41 81 35. 62 9 9 10. 522 3 54. 5 02 /b> 2 10. 144 4 Band 23 .27 97 ... method By method in [17] By proposed method By method in [17] γ=1 γ = 0. 1 25 30 41 . 86 /b> 37 41 .7 722 41 . 80 7 1 40 . 34 20 43 . 20 4 /b> 4 43 . 08 /b> 02 43 . 127 4 41 . 24 /b> 96 Table 2: TMUX system SNRs and SCRs comparison for ... comparison between diﬀerent receiver design approaches Constraint γ 10 15 SNRc (dB) 20 30. 75 18 30. 74 50 30. 747 6 30. 57 84 35.3 3 02 /b> 35.3 100 35.3177 34. 9 161 39 .21 35 39.19 38 39.1 82 8 38. 3 08 /b> 0 SNRr (dB) By...

8
307
0

Part 4: Code of practice for design of composite slabs with profiled steel sheeting ppt

Danh mục: Kiến trúc - Xây dựng

... Tel: 02 /b> 0 89 96 7111 Fax: 02 /b> 0 89 96 7 04 /b> 8 Subscribing members of BSI are kept up to date with standards developments and receive substantial discounts on the purchase price of standards For details of ... of 1 .25 is a partial safety factor for resistances gm, selected on the basis of the behaviour and mode of failure of the slab The empirical parameters mr and kr in this formula should be obtained ... 6. 10 Shear connection © BSI 12- 19 98 10 10 10 10 12 13 13 16 16 16 18 20 20 22 22 23 23 i BS 59 50- 4: 19 94 Page Section Fire resistance 7.1 General 7 .2 Minimum thickness of concrete 7.3 Determination...

38
722
4

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps

Danh mục: Kĩ thuật Viễn thông

... Rate, 42 3 ix CHAPTER Valves, Fittings, and Piping Details 42 5 Valve Types, 42 6 /b> Ball Valves 42 6 /b> , Plug Valves 4 30, Gate Valves 4 32, Butterfly Valves 4 32, Globe Valves 4 32, Diaphragm (Bladder) Valves ... Matrix and Function Charts, 40 6 /b> Symbols, 4 10 Hazards Analysis, 41 8 Types of Hazards Analysis 41 8, Problems Commonly Encountered 41 9 Safety Management Systems, 4 20 Safety Case and Individual Risk Rate, ... psig 4 ,00 0 psig 1 ,00 0 psig 1 20 F 175°F 22 4 F Separator Gas Composition (1 ,00 0 psia) Component CO, N, c, C, C3 i C4 n C4 »C nC, C6 C7+ H2S Mole % 4 .03 1 .44 85 .55 5. 74 1.79 0. 41 0. 41 0. 20 0.13 0. 15...

25
362
0

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 2 doc

Danh mục: Kĩ thuật Viễn thông

... 0. 01 6 02 /b> 0. 01 6 02 /b> 0. 01 6 02 /b> 0. 01 60 3 3 3 06 /b> 29 47 24 /b> 44 20 3 6 .4 1 703 .2 2 947 24 /b> 44 20 3 6 ,4 1 703 .2 00 3 . 02 /b> 8 .05 13 . 06 /b> 18 ,07 60 70 80 90 100 0. 25 63 0. 363 1 05 6 09 06 /b> 8 92 0, 94 92 0. 01 6 04 /b> 0. 01 60 6 0. 01 6 08 /b> 0. 0 16 10 0 .01 61 3 ... 1 .4 325 1 .41 36 1.39 42 1.37 42 1.35 32 500 5 20 5 40 5 60 5 80 60 0 6 20 6 40 6 60 6 80 15 42 . 9 1 7 86 /b> .6 20 5 9.7 23 65 .4 2 7 08 /b> .1 0. 023 6 00 4 27 00 6 20 007 28 /b> 0. 0 305 0. 24 /b> 32 0. 1955 0. 15 38 0. 1 165 0. 08 10 0 . 26 /b> 68 0. 2 20 1 ... 0. 7 86 /b> 8 0. 765 3 1 .47 93 1 .4 700 1 .4 60 6 1 .45 13 1 .44 19 4 50 4 60 4 70 4 80 4 90 500 5 20 5 40 5 60 5 80 6 80 . 8 8 12. 4 9 62 . 5 1133.1 1 325 .8 00 0 24 /b> 00 0 29 0. 021 5 0. 022 1 0. 022 8 0. 6 545 0. 5 385 04 /b> 3 44 0. 3 64 7 0. 29 89 06 /b> 4...

25
383
0

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 3 pps

Danh mục: Kĩ thuật Viễn thông

... 100 ,00 0 2 50, 000 500 ,00 0 7 50, 000 1 ,00 0 ,00 0 1, 500 ,00 0 2 ,00 0 ,00 0 2, 500 ,00 0 3 ,00 0 ,00 0 3, 500 ,00 0 4 ,00 0 ,00 0 5 ,00 0 ,00 0 * Minimum Diameter-in 2. 5 3.9 5.5 6. 7 7 .8 9.5 11 .0 12, 3 13.5 14. 6 15 .6 17 .4 46 ... 100 .00 Sum (Aj) B Molecular Weight C Critical Temp °R D Critical psia 547 .87 107 1 .0 44 .01 0 49 3 .0 28 /b> .01 3 22 7.3 34 .07 6 103 6 .0 6 72. 6 343 .37 16 . 04 /b> 3 66 7 .8 707 .0 30. 0 70 5 50. 09 44 .09 7 61 6. 3 66 6 .01 7 34. 98 ... 7 34. 98 529 58. 1 24 /b> 58. 1 24 /b> 5 50. 7 765 .65 4 90. 4 72. 151 82 9 , 10 48 /b> 8. 6 84 5 . 70 72. 151 86 /b> .1 78 913. 70 43 6. 9 3 04 /b> 147 11 12 .0 19 . 48 /b> 3 74. 6 6 80 . 5 Sum (Aj x B{ ) Sum (A, x Cj) Sum (Aj xDj) Sum (A, ) Sum ( Aj) Sum...

25
348
0

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf

Danh mục: Kĩ thuật Viễn thông

... 25 .00 1 24 /b> 1 48 /b> 1 74 1 16 1 42 166 1 12 1 36 1 60 1 12 1 40 1 62 1 08 /b> 1 38 1 62 48 /b> 60 71 44 56 68 i 84 21 6 25 6 88 100 1 16 88 98 1 16 27 .00 2 .0 90 31 .00 20 9 23 8 27 5 20 2 23 2 26 /b> 4 1 92 2 32 2 64 191 22 1 26 /b> 1 188 21 5 24 /b> 9 ... 1 28 /b> 1 48 /b> 1 68 42 8 /b> 4 92 5 70 42 6 /b> 4 92 566 41 4 48 /b> 4 5 56 1 98 23 6 27 6 1 96 22 8 26 /b> 8 3 .0 90 4 .0 20 45 .00 4 42 522 60 3 42 7 5 06 /b> 583 42 4 500 5 72 42 8 /b> 49 7 575 4 12 48 /b> 4 5 62 40 4 4 72 5 52 195 22 8 27 1 1 90 22 4 26 /b> 4 67 6 ... 5 62 6 40 46 /b> 8 5 48 /b> 6 40 23 6 27 7 3 20 33 .00 35 .00 37 ,00 7 82 89 6 100 4 7 68 8 68 9 78 7 68 8 68 9 64 7 42 84 6 /b> 9 52 7 32 83 1 931 7 32 8 20 9 28 /b> 39 .00 4 .0 20 45 .00 1 1 02 /b> 12X3 1 48 /b> 4 1 06 /b> 2 123 2 1 42 4 1 04 /b> 5 122 2 141 5 4X 00 51...

25
379
0

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 5 pps

Danh mục: Kĩ thuật Viễn thông

... Propane 0. 25 Isobutane 0. 0 04 /b> 1 0. 15 0. 72 0. 0 04 /b> 1 n-Butane Infinity Pentane"1" 0. 0 06 /b> 3 1 .00 00 Total Interpolating linearly, Y/K=1. 0at 74 ]F yn/i 00 0 .00 0. 00 0. 90 0 . 08 /b> 0. 07 0. 03 0. 00 0 .00 J . 08 /b> At ... At 80 F Kn Yn/Sn Infinity Infinity 0. 00 0 .00 0. 00 0 .81 0. 05 0. 00 0 .01 0. 00 0 .00 0. 87 0. 5 05 1 .22 Infinity 0. 6 1 .22 Infinity Figure 4- 5 Approximate hydrate temperature formation (Courtesy of ... is saturated with water vapor, it is by definition at its dew point The amount of water vapor saturated in the gas is given Hydrates 99 Table 4- 1 Calculation of Temperature for Hydrate Formation...

25
351
0

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx

Danh mục: Kĩ thuật Viễn thông

... 10. 3 3. 61 6 1 .00 0 .00 0 42 " » 1 ,00 0 .00 0 42 " « 1 ,00 0 .00 0 42 " * 1 ,00 0 ,00 0 42 " x 4' «" 1. 500 .00 0 48 /b> " * 7 '6" 1, 500 .00 0 4' 4" 2- 2"XH 34 40 93 .4 166 17.9 4 . 06 /b> 0 4' 4" 12- r'XXH 73 40 85 .9 166 17.9 4, 725 WXH 3 20 0 ... 2 60 , 000 24 /b> " > r«" 8 -2- XH 34 40 29 -S S4 2. 9 1. 40 0 2 90. 000 24 /b> " < re~ 8- y'XXH 73 40 26 /b> .5 54 2. 9 1 .6 10 500 ,00 0 30" * 0" 0" 8 -2" XH 34 40 42 . 6 76 6 .0 2, 2 10 500 .00 0 30" x 0- 0" 8 -2" XXH 73 40 38. 3 76 6 .0 2. 5 10 ... 8Std 8XS 8XXS 0. 179 0. 1 54 0. 21 8 0. 43 6 0. 20 3 0. 27 6 0. 5 52 0. 7 50 0 .87 5 0. 21 6 0. 300 0. 60 0 0. 23 7 0. 337 0. 6 74 0. 2 80 0 .4 32 0. 8 64 0. 322 0. 500 0. 87 5 Maximum Working Pressure* Grade B S = 20 , 000 psig 5 ,27 0...

25
473
0

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 7 ppsx

Danh mục: Kĩ thuật Viễn thông

... lOOscf* 0. 13 0. 0 08 /b> 0. 18 Milligrams per m3* 0, 001 10 0 .63 14. 41 0, 005 50 3.15 72 .07 0. 01 100 6. 30 144 . 14 0. 02 20 0 12. 59 28 /b> 8 . 06 /b> 0. 05 500 31 .49 7 20 . 49 0. 07 700 44 . 08 /b> 100 8. 55 100 0+ 62 . 98 14 40 . 98+ 0. 10+ ... Pressure At !00 °F psia 500 0 80 0 1 90 72. 2 51 ,6 20 . 4 15 .6 5 .0 - ~0. 1 — — 3 94 Relative Volatility 96, 9 15.5 3. 68 1. 40 1 .00 0. 40 0. 30 0. 10 0 .00 Infinite Infinite 7. 64 (equation continued from page 1 38) ... sulfide = 62 9 .77 gr/ 100 scfat 14. 69 6 psia and 59°F, or 101 , 325 kPa and 75°C Acid Gas Treating 1S3 ening At 500 ppm, H2S can no longer be smelled, but breathing problems and then death can be expected...

25
391
0

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 8 doc

Danh mục: Kĩ thuật Viễn thông

... and carbon disulfide (CS2) to form heat-stable salts that cannot be regenerated At temperateres above 24 /b> 5 °F a side reaction with CO2 exists that produces oxazolidone -2, a heat-stable salt, and ... temperature rise in the absorber The solution concentration for a potassium carbonate system is limited by the solubility of the potassium bicarbonate (KHCO3) in the rich 1 68 Design of GAS-HANDLING ... with 0% retained on 16 mesh, 80 % between 30 and 60 mesh, and 100 % retained on 325 mesh It is purchased with a moisture content of 20 % by weight and buffering to meet a flood pH of 10 Because it is...

25
403
0

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 9 pdf

Danh mục: Kĩ thuật Viễn thông

... content for a natural gas with a molecular weight of 26 /b> that is in equilibrium with a 3% brine at a pressure of 3 ,00 0 psia and a temperature of 1 50 R From Figure 8- 1 at a temperature of 1 50 F and ... inlet gas increases as the inlet gas temperature increases For example, at 1 ,00 0 psia and 80 F gas holds about 34 Ib/MMscf, while at 1 ,00 0 psia and 1 20 F it will hold about 1 04 /b> Ib/MMscf At the higher ... Total acid gas inlet = 4 .03 + 0. 001 9 = 4 .03 2% Pacidin = 1 .01 5 x (4 .03 2/ 100 ) = 40 . 9 psia Total acid gas outlet = 2 .0% Pa«d out = 1 ,01 5 x (2 .0/ 100 ) = 20 . 3 psia From Figure 7- 12 for removing CO2 and...

25
438
0

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 10 pdf

Danh mục: Kĩ thuật Viễn thông

... extradate 0. 05 60 0 .07 22 0. 1 52 0. 23 8 0. 000 088 9 0. 000 1 24 /b> 0. 000 1 36 0. 000 2 10 Pressure drops of greater than approximately psi are not recommended Moisture Content of Inlet Gas An important variable ... f/gal 300 40 0 500 60 0 700 80 0 900 100 0 1 100 1 20 0 1 300 1 40 0 1 500 1.7 2. 3 2. 8 3 .4 3.9 4. 5 5 .0 5 .6 6.1 6. 7 7 .2 7.9 8. 3 Contactor Operating Pressure EXAMPLE 8- 1: GLYCOL DEHYDRATION Problem: Calculate ... 8 -2 Approximate Reboiler Heat Duty Design Gallons of Glycol Circulated /Ib H2O Removed Reboiler Heat Duty Btu/Gal of Glycol Circulated 2 .0 2. 5 3 .0 3.5 4 .0 4. 5 5 .0 5.5 6 .0 1 06 /b> 6 943 8 62 80 5 762 ...

25
446
0

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx

Danh mục: Kĩ thuật Viễn thông

... Number Actual Trays Below Main Feed Number 20 0 -1 100 24 /b> - 30 20 - 50 4 50- 60 0 20 - 30 20 - 50 175- 300 85 -1 60 24 /b> - 30 2- 60 20 - 50 16- 60 5 50- 6 50 3 50- 500 20 0 - 300 70- 100 14- 30 10- 70 17- 70 18- 70 26 /b> - 30 20 - 70 18- 70 ... Grade 22 -25 Grade 18 -25 Grade 14 -25 40 i Grade 34- 40 Grade 30- 40 Grade 26 /b> - 40 Grade 22 - 40 Grade 18- 40 Grade 14- 40 55 i Grade Grade Grade Grade Grade 70 i 34- 55 30- 55 26 /b> -55 22 -55 18- 55 Grade 14- 55 85 ... -37* ASTMD- 183 7 -81 2. 5 — — 2, 5 ASTMD -2 163 - 82 2 .0 2 .0 — ASTM D -2 163 - 82 — — — — ASTMD -2 1 58- 80 ASTM D -21 58- 80 ASTMD- 183 8- 84 ASTM D -27 84 - 80 I GPA Propane Dryness Test (Cobalt Bromide) or D -27 ...

25
459
0

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 2 pps

Danh mục: Kĩ thuật Viễn thông

... Integral (onshore only) 10 20 2 .0 2. 7 2, 7 ! 3 4 40 9 80 3,9 20 High Speed High Speed Centrifugal 100 2 2.7 2 .0 2 .0 2 .0 2 19, 6 02 /b> 88 1 90 3 80 Centrifugal Screw High Speed High Speed High Speed Screw 4 .0 ... horsepower and number of stages A first approximation of the number of stages can be made by assuming a maximum compressor ratio per stage of 3 ,0 to 4 .0 and choosing the number of stages such that: ... can be assumed that ratio per stage is equal for each stage • Next, calculate the discharge gas temperature for the first stage If the discharge temperature is too high (more than 300 °F), a large...

25
351
0

a spr sensorgrams for different concentrations of glyphosate 0 2 4 8 16 32 and 64 μm the sensor chip is modified with p1 cys with a surface density of 0 6 molecule nm2 b spr responses at various glyphosate concentrations the